2022
DOI: 10.5194/gmd-15-7139-2022
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MultilayerPy (v1.0): a Python-based framework for building, running and optimising kinetic multi-layer models of aerosols and films

Abstract: Abstract. Kinetic multi-layer models of aerosols and films have become the state-of-the-art method of describing complex aerosol processes at the particle and film level. We present MultilayerPy: an open-source framework for building, running and optimising kinetic multi-layer models – namely the kinetic multi-layer model of aerosol surface and bulk chemistry (KM-SUB) and the kinetic multi-layer model of gas–particle interactions in aerosols and clouds (KM-GAP). The modular nature of this package allows the us… Show more

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Cited by 9 publications
(10 citation statements)
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“…The characteristic time for transport of OH radicals to the interface is d 2 π 2 D , where d = 2.5 nm (the approximate size of the DSPC molecule at the air–water interface) and an estimate of the diffusion coefficient D = 2.8 × 10 –9 m 2 s –1 gives ∼0.2 ns. The characteristic reaction time is 1 k where k = 3.5 × 10 –4 s –1 taken from Table which gives a value with respect to reaction at the interface as ∼3000 s. A detailed mass-transfer calculation or multilayer diffusion model as described elsewhere , is thus not considered. The photolytic source of OH radicals from an enormous excess of nitrate anions was chosen to prevent a diffusive concentration profile from building up to the interface over the course of the long reaction time.…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…The characteristic time for transport of OH radicals to the interface is d 2 π 2 D , where d = 2.5 nm (the approximate size of the DSPC molecule at the air–water interface) and an estimate of the diffusion coefficient D = 2.8 × 10 –9 m 2 s –1 gives ∼0.2 ns. The characteristic reaction time is 1 k where k = 3.5 × 10 –4 s –1 taken from Table which gives a value with respect to reaction at the interface as ∼3000 s. A detailed mass-transfer calculation or multilayer diffusion model as described elsewhere , is thus not considered. The photolytic source of OH radicals from an enormous excess of nitrate anions was chosen to prevent a diffusive concentration profile from building up to the interface over the course of the long reaction time.…”
Section: Resultsmentioning
confidence: 99%
“…Characteristic time scales for diffusion and reaction can be estimated from simple formulas in Finlayson-Pitts and Pitts. 84 The characteristic time for transport of OH radicals to the interface is d 1 which gives a value with respect to reaction at the interface as ∼3000 s. A detailed mass-transfer calculation or multilayer diffusion model as described elsewhere 86,87 is thus not considered. The photolytic source of OH radicals from an enormous excess of nitrate anions was chosen to prevent a diffusive concentration profile from building up to the interface over the course of the long reaction time.…”
Section: •−mentioning
confidence: 99%
“…Recent developments in multilayer modeling include the incorporation of film growth mechanisms, the treatment of the lung epithelial lining fluid to derive health implications from these models, , an educational tool, and a move toward machine learning algorithms . We have recently published open-source software, MultilayerPy, which facilitates the creation and optimization of these models . MultilayerPy is free for anyone to use and has the potential to incorporate current and future multilayer models.…”
Section: Techniques Usedmentioning
confidence: 99%
“…Kinetic multilayer modeling has helped us describe the impact of surfactant self-organization on processes at the aerosol and film levels. The recent development of MultilayerPy and methods to analyze the output of these models has increased the accessibility and interpretability of this kind of modeling. There is a need to efficiently link these computationally expensive models with large-scale atmospheric models that consider aerosols .…”
Section: Summary and Future Workmentioning
confidence: 99%
“…We have devised a multi-layer approach to spatially and temporally resolve the uptake and diffusion of water through a self-assembled particle, incorporating changes in diffusivity caused by water content-dependent phase changes. This modelling approach is similar to those which resolve aerosol and surface and bulk chemistry [34][35][36][37][38] and ones which consider water uptake into viscous particles. 4,20,39 The multi-layer model is described in detail in the ESI †.…”
Section: Multi-layer Water Uptake Modelmentioning
confidence: 99%